CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

Biomass Gasification

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   October 4, 2007, 10:55
Default Biomass Gasification
  #1
Antonio Oliveira
Guest
 
Posts: n/a
Dear Fluent Users.

I am a Brazilian student and I started a PhD at Aston University - UK this year. I intend to use Fluent to simulate a Downdraft Biomass Gasification Process, but I am new in CFD's World and I need some advice. Then, I will appreciate if anyone give me some advice.

My best Wishes.

Antonio Oliveira
  Reply With Quote

Old   October 4, 2007, 12:33
Default Re: Biomass Gasification
  #2
Allan Walsh
Guest
 
Posts: n/a
What aspects are you working on? The built in models of Fluent probably are fine if you are interested in flows, temperatures, etc. If you need to do more detailed chemistry of gasification you will need to implement your own code. Writing UDFs can be time consuming - allow several weeks or months for each.
  Reply With Quote

Old   October 7, 2007, 12:13
Default Re: Biomass Gasification
  #3
Antonio Oliveira
Guest
 
Posts: n/a
Thanks.

I am interested in study the species and temperature profiles. I am interested in the pressure drop across the bed too. I think that I will need to write UDF's. What do you suggest?
  Reply With Quote

Old   October 8, 2007, 15:06
Default Re: Biomass Gasification
  #4
Allan Walsh
Guest
 
Posts: n/a
On the pressure drop, you probably want to consider porous cells, although this approach is more of a parametric analysis. The porous cells can give reasonable agreement with measured pressure losses but don't give much information about packing density or influence of gasification rates, etc. You may wish to consider a two-phase fluid approach, but this is a major project.

Will you have experimental data on which to base your reaction rates? If not, I would suggest that writing UDFs for the reactions would not be worth it.

Good luck.

  Reply With Quote

Old   October 8, 2007, 17:02
Default Re: Biomass Gasification
  #5
Antonio Oliveira
Guest
 
Posts: n/a
Dear Allan Walsh,

Thanks for your help. I will star the activities and follow your advice.

Best wishes.

Antonio Oliveira
  Reply With Quote

Old   November 26, 2009, 04:15
Default
  #6
New Member
 
Wang Long
Join Date: Sep 2009
Posts: 5
Rep Power: 17
wanglong is on a distinguished road
Quote:
Originally Posted by Allan Walsh
;146012
On the pressure drop, you probably want to consider porous cells, although this approach is more of a parametric analysis. The porous cells can give reasonable agreement with measured pressure losses but don't give much information about packing density or influence of gasification rates, etc. You may wish to consider a two-phase fluid approach, but this is a major project.

Will you have experimental data on which to base your reaction rates? If not, I would suggest that writing UDFs for the reactions would not be worth it.

Good luck.
Dear Allan
I also tried to build a biomass gasification model use Fluent6.3
Could you talk about how to set two phase reactions?
It is fixed bed, how to set biomass particles as fixed and slowly drop down in the gasification process?
Thank you!

Wang
wanglong is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
biomass gasification simulation anbuvrp STAR-CCM+ 4 April 29, 2011 10:36
Biomass Gasification Sudhahar Siemens 4 November 26, 2009 04:22
Problems bout CFD model of biomass gasification, Downdraft gasifier wanglong FLUENT 2 November 26, 2009 00:27
Biomass Gasification Antonio Oliveira CFX 1 October 8, 2007 19:24
Biomass gasification rayy FLUENT 0 January 12, 2007 16:06


All times are GMT -4. The time now is 01:27.